CN108439476B - Preparation of low-valence manganese oxide, product and synthetic lithium ion sieve precursor L i1.6Mn1.6O4Application of - Google Patents
Preparation of low-valence manganese oxide, product and synthetic lithium ion sieve precursor L i1.6Mn1.6O4Application of Download PDFInfo
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- CN108439476B CN108439476B CN201810368209.1A CN201810368209A CN108439476B CN 108439476 B CN108439476 B CN 108439476B CN 201810368209 A CN201810368209 A CN 201810368209A CN 108439476 B CN108439476 B CN 108439476B
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- C01G45/00—Compounds of manganese
- C01G45/12—Manganates manganites or permanganates
- C01G45/1207—Permanganates ([MnO]4-) or manganates ([MnO4]2-)
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Abstract
The invention discloses a preparation method of low-valence manganese oxide, a product and synthesis L i1.6Mn1.6O4The use of (1), the preparation of the low-valent manganese oxide comprises: mixing manganese dioxide with a liquid-phase organic reducing agent, and preparing the mixture by a chemical reduction method; the low valence manganese-oxygen mixture comprises a mixture of manganous-manganic oxide, manganous oxide, manganese oxyhydroxide and part of unreduced manganese dioxide, and the average valence of manganese elements of the mixture is between 3.01 and 3.55. The invention reduces the manganese dioxide into a mixture of low-valence manganese oxide compounds by using an active liquid-phase organic micromolecular reducing agent to react with the manganese dioxide raw material under hydrothermal conditions. Compared with the traditional method, the process does not need high-temperature roasting, and is a clean production process with mild conditions, high efficiency and low energy consumption. Has the characteristics of energy conservation and low cost.
Description
Technical Field
The invention belongs to the field of energy-saving production of inorganic compounds, and particularly relates to preparation and product of low-valence manganese oxide and synthesized lithium ion sieve precursor L i1.6Mn1.6O4The use of (1).
Background
MnO2The compound is an oxidant with mild property, can oxidize active alcohol hydroxyl into aldehyde or ketone under neutral or alkaline condition, wherein the allyl and benzyl alcohol are most active, and can react at room temperature under the neutral condition to be oxidized into aldehyde. However, during the production and storage of industrial manganese dioxide, the surface of manganese dioxide powder is deactivated and oxygen is lostChemical capacity, resulting in the difficult efficient redox reaction of manganese dioxide with alcohol, and lithium manganese oxide lithium ion sieve precursor L i1+xMn2-xO4In the synthesis, the valence state of manganese is 3-4, and the synthesis of the ion sieve usually requires the use of a low-valence oxide of manganese, such as trivalent manganese oxide Mn2O3Manganese oxyhydroxide MnO (OH), manganomanganic oxide Mn3O4And the like.
In the methods provided in most patents, manganese oxide and manganese dioxide are obtained by high temperature roasting of manganese dioxide for decomposition. In the preparation method of the CN107138126A lithium ion sieve adsorbent and the method for adsorbing lithium ions, step 1, weighing a manganese-containing compound and a lithium-containing compound in a mass ratio of 6: 1-14: 1, uniformly mixing in a crucible, roasting in a muffle furnace at 400-1000 ℃ for 60-300 min, cooling to room temperature, and grinding to obtain a lithium type ion sieve; the manganese-containing compound is manganese dioxide, so that the high-temperature reaction has high energy consumption, pollutes the environment and is not environment-friendly;
for example, "CN 101264935A A method for reducing MnO in anode mud by high-temp2The method for reducing MnO comprises the following steps: uniformly mixing electrolytic manganese anode mud and a reducing agent in a reaction device, reacting for 1-6 h at 800-1600 ℃, naturally cooling to room temperature under the protection of nitrogen and reducing atmosphere to obtain a mixed product containing MnO particles, and directly returning the product to electrolytic manganese metal production to be used as a raw material or further separating and purifying to obtain an MnO product.
For another example: patent "CN 103121724B A method for preparing lithium ion sieve MnO2·0.5H2O and its precursor L i1.6Mn1.6O4The method gives a precursor L i which is obtained by taking inorganic manganese salt and lithium salt as raw materials, carrying out one-step hydrothermal synthesis on an intermediate, and then roasting at a low temperature1.6Mn1.6O4Then, the precursor is subjected to acid treatment to extract L i in the precursor to form an H-type ion sieve, and the H-type ion sieve is washed, filtered and dried to obtain the ion sieve adsorbent MnO with the lithium ion sieving effect2·0.5H2O, i.e. reaction of potassium permanganate with manganous saltPreparation L i1.6Mn1.6O4And the amount of waste water generated in the reaction process is large, which is not beneficial to the environmental protection in the later period.
It can be seen that in the patents relating to the preparation of lithium manganese oxide lithium ion sieves from manganese dioxide, the required low valence manganese oxide is prepared by high temperature decomposition or by reacting a divalent manganese salt with a large amount of an inorganic oxidant such as potassium permanganate to obtain an intermediate valence manganese oxide compound. High energy consumption, large amount of waste water and high production cost.
Disclosure of Invention
Aiming at the defects and shortcomings of the prior preparation technology, the invention aims to provide a preparation method of low-valence manganese oxide, a product and a synthetic lithium ion sieve precursor L i1.6Mn1.6O4The process does not need high-temperature roasting, and is a clean production process with mild conditions, high efficiency and low energy consumption.
In order to achieve the purpose, the invention adopts the following technical scheme:
a low-valent manganese oxide, the preparation of which comprises: mixing manganese dioxide with a liquid-phase organic reducing agent, and preparing the mixture by a chemical reduction method;
the low-valence manganese oxide comprises a mixture of trimanganese tetroxide, manganic oxide, manganese oxyhydroxide and manganese dioxide, and the average valence state of the manganese element of the low-valence manganese oxide is 3.01-3.55.
The preparation method of low-valence manganese oxide comprises the steps of mixing manganese dioxide with a liquid-phase organic reducing agent, and preparing the mixture by a chemical reduction method;
the amount of the liquid-phase organic reducing agent is 1-3 times of that of the manganese dioxide raw material.
Optionally, the liquid-phase organic reducing agent is one or more of primary alcohol, allyl alcohol and benzyl alcohol containing active hydroxyl groups.
Optionally, mixing manganese dioxide and a liquid-phase organic reducing agent, placing the mixture in a high-pressure reaction kettle, carrying out hydrothermal reaction for 12-24 h at 120-140 ℃, cooling along with a furnace, filtering to remove residual liquid organic mixture and water, and drying the solid to obtain the low-valence manganese-oxygen mixture.
The low-valence manganese oxide is prepared by the preparation method of the low-valence manganese oxide.
Low-valence manganese oxide or low-valence manganese oxide prepared by the preparation method of low-valence manganese oxide is used for preparing manganese ferrite lithium ion sieve precursor L i1.6Mn1.6O4The use of (1).
Compared with the prior art, the invention has the beneficial effects that:
the method reduces the manganese dioxide into a mixture of low-valence manganese oxide compounds by using an active liquid-phase organic micromolecule reducing agent to react with the manganese dioxide raw material under mild heterogeneous conditions. Compared with the traditional method for obtaining manganese sesquioxide by decomposing manganese dioxide at high temperature of 1100 DEG C
In comparison, the process does not need high-temperature roasting, and is a clean production process with mild conditions, high efficiency and low energy consumption. Has the characteristics of energy conservation and low cost.
Detailed Description
The following embodiments of the present invention are provided, and it should be noted that the present invention is not limited to the following embodiments, and all equivalent changes based on the technical solutions of the present invention are within the protection scope of the present invention.
Example 1:
(1) accurately weighing 50gMnO2(analytically pure, Komeo) sample, determining the manganese content to be 95.20% by EDTA titration method, adding 200m L absolute ethyl alcohol, magnetically stirring the mixture in a high-pressure hydrothermal reaction kettle with a polytetrafluoroethylene lining kettle until the mixture is uniform, adding a stainless steel outer sleeve for sealing, placing the mixture in a 120 ℃ oven for heating reaction for 24 hours, taking out the mixture and cooling the mixture to room temperature, and drying the obtained viscous liquid mixture at the normal pressure of 80 ℃ for 6 hours to obtain 49.80 g of low-valence manganese oxide mixture.
(2) Accurately weighing 0.5g of the mixture obtained in the step (1), mixing and heating the mixture by using a proper amount of 1/1 hydrochloric acid and a small amount of water until the sample is completely dissolved and residual Cl in a yellow-green solution is formed2Drive off and transfer the solution to a 250m L capacityDiluting to a scale mark in a bottle, shaking up, transferring 25.00m L by using a pipette, adding 10m L of ammonia/ammonium chloride buffer solution with the pH value of 10 and 0.15g of hydroxylamine hydrochloride, stirring and dissolving, adding 5 drops of K-B indicator, dropping EDTA standard solution with known accurate concentration until the solution is pure blue, carrying out 3 experiments in parallel, and calculating the content of Mn in the sample to be 95.20% according to the formula (1).
(3) Accurately weighing 0.1005g of the mixture of low valence manganese oxides of (1) in a 250m L conical flask, adding Na with known accurate concentration2C2O4The standard solution 25.00m L was diluted with 15m L deionized water and shaken well, then 10m L of 3 mol/L sulfuric acid was added, placed on a water bath at 80 ℃ and heated until the sample was completely dissolved, and KMnO of known precise concentration was used while hot4Back titration of unreacted Na from standard solution2C2O4The average valence of manganese in the low-valence manganese oxide is 3.01 by the following formula (2) through 3 parallel experiments.
(4) Mixing the manganese oxide with lithium-containing inorganic powder (lithium hydroxide) according to the lithium-manganese ratio of 1/1, and preparing a lithium manganese oxide lithium ion sieve precursor L i by a high-temperature solid phase method (refer to the preparation method of CN107138126A lithium ion sieve adsorbent and the method of absorbing lithium ions)'1.6Mn1.6O4After low-acid delithiation, the solution was adsorbed for 10 hours in an aqueous environment containing 0.2 g/L of lithium ions at pH 10 to reach equilibrium, and the amount of adsorbed lithium was found to be 25.3 mg/g.
Example 2:
(1) accurately weighing 50gMnO2(analytically pure, Komeo) sample, adding 200m L allyl alcohol, magnetically stirring in a polytetrafluoroethylene lined kettle of a high-pressure hydrothermal reaction kettle until uniform, sealing with a stainless steel jacket, heating in a 120 ℃ oven for reaction for 24h, taking out, and cooling to room temperatureAfter the temperature is raised, the obtained viscous liquid mixture is dried for 12 hours at the normal pressure of 60 ℃ to obtain 49.70g of a mixture of low-valence manganese oxides.
(2) The content of manganese in the product was measured in the same manner as in (2) in example 1, and the content of Mn in the mixture was measured to be 95.24%.
(3) The valence of manganese in the product was determined in the same manner as in (3) in example 1, and the average valence of manganese in the lower manganese oxide was found to be 3.05.
(4) Lithium manganese oxide lithium ion sieve precursor L i prepared and obtained by using product and lithium-containing inorganic powder1.6Mn1.6O4The preparation method was the same as that of (4) in example 1, and after equilibrium was reached by adsorption for 8 hours, the amount of adsorbed lithium was 21.4 mg/g.
Example 3:
(1) accurately weighing 50gMnO2(analytically pure, Komeo) sample is added with 100m L absolute ethyl alcohol, the mixture is magnetically stirred in a polytetrafluoroethylene lining kettle of a high-pressure hydrothermal reaction kettle until the mixture is uniform, a stainless steel outer sleeve is added for sealing, the mixture is placed in a 120 ℃ oven for heating reaction for 24 hours, the mixture is taken out and cooled to room temperature, and the obtained viscous liquid mixture is dried for 6 hours at the normal pressure of 80 ℃ to obtain 49.60g of low-valence manganese oxide mixture.
(2) The content of manganese in the product was measured in the same manner as in (2) in example 1, and the content of Mn in the mixture was measured to be 95.22%.
(3) The valence of manganese in the product was determined in the same manner as in (3) in example 1, and the average valence of manganese in the lower manganese oxide was found to be 3.55.
(4) Lithium manganese oxide lithium ion sieve precursor L i prepared and obtained by using product and lithium-containing inorganic powder1.6Mn1.6O4The preparation method was the same as that of (4) in example 1, and after equilibrium was reached by adsorption for 8 hours, the amount of adsorbed lithium was 21.2 mg/g.
Example 4:
(1) accurately weighing 50gMnO2(analytically pure, Koimeu) sample, adding 300m L benzyl alcohol, magnetically stirring in a polytetrafluoroethylene lined kettle of a high-pressure hydrothermal reaction kettle until the mixture is uniform, and sealing with a stainless steel outer sleeveThe mixture is put in a baking oven with the temperature of 140 ℃ for heating reaction for 28 hours, and after the temperature of the mixture is reduced along with the furnace, the obtained viscous liquid mixture is dried for 6 hours at the temperature of 80 ℃ under normal pressure, and 49.56g of mixture of low-valence manganese oxide is obtained.
(2) The content of manganese in the product was measured in the same manner as in (2) in example 1, and the content of Mn in the mixture was measured to be 95.34%.
(3) The valence of manganese in the product was determined in the same manner as in (3) in example 1, and the average valence of manganese in the lower manganese oxide was found to be 3.01.
(4) Lithium manganese oxide lithium ion sieve precursor L i prepared and obtained by using product and lithium-containing inorganic powder1.6Mn1.6O4The preparation method was the same as that of example 1, and the amount of adsorbed lithium was 25.12mg/g, as measured after 6 hours.
The preferred embodiments of the present disclosure have been described in detail above, however, the present disclosure is not limited to the specific details of the above embodiments, and various simple modifications may be made to the technical solution of the present disclosure within the technical idea of the present disclosure, and these simple modifications all fall within the protection scope of the present disclosure.
It should be noted that, in the foregoing embodiments, various features described in the above embodiments may be combined in any suitable manner, and in order to avoid unnecessary repetition, various combinations that are possible in the present disclosure are not described again.
In addition, any combination of various embodiments of the present disclosure may be made, and the same should be considered as the disclosure of the present disclosure, as long as it does not depart from the spirit of the present disclosure.
Claims (1)
1. Low-valence manganese oxide used for preparing manganese oxide lithium ion sieve precursor L i1.6Mn1.6O4Characterized in that the preparation of the low-valent manganese oxide comprises: mixing manganese dioxide with a liquid-phase organic reducing agent, and preparing the mixture by a chemical reduction method;
the organic reducing agent is benzyl alcohol, the adding amount of manganese dioxide is 50g, and the adding amount of the benzyl alcohol is 300m L;
mixing manganese dioxide and a liquid-phase organic reducing agent, placing the mixture in a high-pressure reaction kettle, carrying out hydrothermal reaction for 28h at 140 ℃, cooling along with a furnace, filtering to remove residual liquid organic mixture and water, and drying the obtained viscous liquid mixture for 6h at the normal pressure of 80 ℃ to obtain a low-valence manganese-oxygen mixture;
the average valence of the manganese element of the low valence manganese-oxygen mixture is 3.01.
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Citations (3)
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JPS59223236A (en) * | 1983-06-02 | 1984-12-15 | Chuo Denki Kogyo Kk | Production of high purity manganese compound |
CN106745285A (en) * | 2017-03-01 | 2017-05-31 | 哈尔滨工业大学 | A kind of α MnO2The preparation method of nano wire |
CN107138126A (en) * | 2017-07-18 | 2017-09-08 | 河北工程大学 | A kind of preparation method of lithium ion sieve adsorbant and the method for adsorbing lithium ion |
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JPS59223236A (en) * | 1983-06-02 | 1984-12-15 | Chuo Denki Kogyo Kk | Production of high purity manganese compound |
CN106745285A (en) * | 2017-03-01 | 2017-05-31 | 哈尔滨工业大学 | A kind of α MnO2The preparation method of nano wire |
CN107138126A (en) * | 2017-07-18 | 2017-09-08 | 河北工程大学 | A kind of preparation method of lithium ion sieve adsorbant and the method for adsorbing lithium ion |
Non-Patent Citations (1)
Title |
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Low temperature preparation of nanocrystalline Mn2O3 via ethanol-thermal reduction of MnO2;wenliang He et al.;《Journal of Crystal Growth》;20031231;285-288 * |
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